Sustainable process recovers ultra high- purity styrene from waste polystyrene
produced will more than likely require blending with conventional styrene to dilute the presence of certain impuri- ties that cannot be removed by distilla- tion alone. Examples of such impurities have been cited in preceding sections. In case any of the co-boiling impurities turn out to be higher than designed, the blending approach will fail due to the requirement of large extra conven- tional styrene volumes. This also has an impact on any future plans for scale-up of recycled PS production by a client. In the case of the SuRe styrene process, due to the usage of crystallisation at the back end, there is no requirement for blending since all these impurities are removed with ease. • In principle, a client can produce a 100% recycled PS product with this technol- ogy as opposed to producing, say, a 10-20% recycled PS product via the blending approach. This will have appeal if a premium for recycled PS develops in the future due to upcoming legislations in waste plastics. Market surveys done in the EU subcontinent indicate that the consumer has an inclination and is will- ing to pay for higher recycled content in plastics, up to an extent of 10% pre- mium in pricing. • The highest-grade PS can be produced since the styrene monomer will meet the most stringent standards. >99.95 wt% styrene with all other impurities below ASTM levels can be achieved and offered as process guarantees. • If the PS recycling facility is located adja- cent to a downstream polymerisation facility, PS purges from the downstream polymerisation section can also be co- fed along with the PS pyrolysis oil in the SuRe styrene process. The styrene can be recovered from the PS purge, which is otherwise lost as fuel oil stream since the purge contains co-boiling impurities like o-xylene. • Barring the distillation energy require- ments, the dominant utility in the back- end crystallisation section is electricity. Considering the present emerging trend of decarbonisation via electrification, the styrene produced from the SuRe process will not only be recycled but also decarbonised if renewable electric- ity is available at the site. The distillation energy requirements are almost entirely met by fuel gas production from the upstream pyrolysis process.
Polystyrene (PS) chemical recycling, as opposed to mechanical recycling, is an emerging route to establish circularity in PS and qualify the recycled PS for strin- gent applications like food-grade PS. To promote this circularity, the crude pyroly- sis oil produced from the depolymerisation section needs to undergo styrene purifica- tion to produce an ASTM qualified styrene monomer for downstream polymerisation. The value chain of polystyrene chemical recycling involves the following three main steps: a) Sorting, b) Depolymerisation, and c) Styrene purification (see Figure 1 ). There is a need to have a tailored styrene purification scheme because the crude pyrolysis oil, obtained from the depoly- merisation section, can contain impuri- ties that either co-boil or close boil with styrene monomer and cannot or are diffi- cult to remove by conventional distillation, resulting in failure of ASTM specification. Examples of such impurities are o-xylene, phenyl acetylene, 1-nonene, oxygenates, sulphur, chlorinated, nitrogenated, close boilers like ethyl benzene, and cumene. These impurities can stem either from the waste PS feedstock wherein, despite the usage of state-of-the-art sorting methods, unwanted plastics may still be present, or the depolymerisation section wherein such impurities can be produced. Hence, there is a need to have a robust styrene purifi- cation solution that can accommodate the removal of such impurities. Sulzer Chemtech is pleased to present its SuRe™ styrene purification technology (see Figure 2 ), which overcomes the issues as stated earlier. It is a hybrid technology wherein distillation is coupled with crystal- lisation at the back end. During the distil- lation process, an impure styrene stream purity is produced and fed into the crystal- lisation section at the back end. The crys- tallisation section offers the following key advantages: 1 The bulk removal of the close boil- ers, such as ethyl benzene, cumene, etc, is done in the distillation section. However, the fine removal, in which there is a disproportionate distillation energy requirement to meet ASTM lev- els, is accomplished via crystallisation at a significantly less energy penalty. This is because melting energy is much less than boiling energy. 2 All co-boilers, like o-xylene, phenyl acet- ylene, etc, are removed to below ASTM acceptable limits. In addition, crystal- lisation removes other impurities like
Pyrolysis/ catalytic/ microwave
Waste PS Quality
Figure 1 Value chain of polystyrene chemical recycling
Capex and Opex attractive, but is immune to feedstock impurities or upsets, which can pose a concern if only conventional distillation is used as a solution. The key value propositions of SuRe styrene purifi- cation are: • Variability in PS waste has no impact on styrene quality that is produced • Co-boiling impurities, such as o-xylene, phenyl acetylene, and 1-nonene, do not impact the final styrene quality. These impurities can come from waste or the depolymerisation process. Further, the unit operation takes care of oxygenate DID YOU KNOW the SURE styrene process is a hybrid technology wherein distillation is coupled with crystallisation at the back end? removal too. Also, the cryogenic nature of the process avoids any polymerisation issues with styrene. • The styrene produced requires no blending. In the case of a distillation- only configuration, the recycled styrene
oxygenates, sulphur, chlorinated, bromi- nated, and nitrogenated species. Melt crystallisation is a method for puri- fication of styrene. A crystalline layer grows from melt on a cooled heat trans- fer surface. The driving force for the crys- tallisation results from the net effect of temperature gradient across the solid and liquid phases. Under these condi- tions, the crystal growth rate is 10 to 100 times faster than in suspension crystalli- sation. Impurity-rich melt is drained from the layer by sweating, and liquid styrene is recovered by melting the crystal layer. Centrifuges, filters or wash columns are not used for solid/liquid separation. New developments allow optimisation of the SuRe styrene process for maximum purity and yield and overall plant economy. Main features are • High yield • Environmentally friendly, no use of solvents • Fewer operating personnel required • Flexibility when dealing with varying feedstock qualities • Short product change over times with no loss of throughput • Flexible adjustment of final product quality • Investment cost savings due to opti- mised process integration • Energy cost savings due to opti- mum combination of distillation and crystallisation • Maintenance cost savings due to the use of proven equipment Thus, the overall solution is not only
C stream 7-
Slipped close boiling non-styrenic impurities like ortho-xylene, colour, oxygenates, sulphur, organo-chlorinated and organo-nitrogenated species, etc.
Ultra high purity styrene (>99.95wt%)
PS Pyrolysis oil
>98% styrene recovery
C stream 9+
Figure 2 SuRe styrene schematic
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